JP4537917B2 - Sedimentation basin equipment - Google Patents

Sedimentation basin equipment Download PDF

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JP4537917B2
JP4537917B2 JP2005262181A JP2005262181A JP4537917B2 JP 4537917 B2 JP4537917 B2 JP 4537917B2 JP 2005262181 A JP2005262181 A JP 2005262181A JP 2005262181 A JP2005262181 A JP 2005262181A JP 4537917 B2 JP4537917 B2 JP 4537917B2
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rectifying
water
settling
inclined plate
sedimentation basin
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俊一 吉元
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荏原エンジニアリングサービス株式会社
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本発明は、浄水場で使用される沈殿池設備に関し、特に沈殿池設備の沈殿池に配置された傾斜板又は傾斜管沈降装置に流入する水の流速を均一化して、沈殿池内のフロックのキャリオーバを防止するようにした沈殿池設備に関するものである。   The present invention relates to a sedimentation basin facility used in a water purification plant, and in particular, uniforms the flow rate of water flowing into a sloping plate or a sloping pipe sedimentation device disposed in the sedimentation basin of the sedimentation basin facility, thereby carrying over the flock in the sedimentation basin. The present invention relates to a sedimentation basin facility that is designed to prevent the above.

従来、この種の沈殿池設備は図1に示すように、沈殿池100内に傾斜板又は傾斜管沈降装置101を配置し、傾斜板又は傾斜管沈降装置101の上部に集水トラフ102、下部に水(濁っている水)の流入する流入室103を配置している。沈殿池100の側部には整流壁104を配置し、該整流壁104を通して水Wが整流されて流入するようになっている。該流入室103に流入した水は傾斜板又は傾斜管沈降装置101の下端流入部に流入する。傾斜板又は傾斜管沈降装置101内においては、流入水は固液分離されて、水は上昇して集水トラフ102に流れ込む。流水中の汚泥は傾斜板又は傾斜管沈降装置101内で分離され、傾斜面を滑り落ち、流入室103を沈降し、該流入室103の底部に堆積する。堆積したフロック、即ち汚泥は汚泥掻寄機108で掻き寄せられ排泥ピット105に集められる。排泥弁106を開くことにより、排泥ピット105内の汚泥は沈殿池100の外に排出されるようになっている。なお、図1の107は、汚泥掻寄機108を駆動する駆動装置である。
水道施設設計指針2000 197ページ 平成12年3月31日発行 社団法人日本水道協会
Conventionally, as shown in FIG. 1, this type of sedimentation basin equipment has an inclined plate or inclined pipe settling device 101 disposed in the settling basin 100, and a water collection trough 102 and a lower portion are disposed above the inclined plate or inclined tube settling device 101. An inflow chamber 103 into which water (turbid water) flows is arranged. A rectifying wall 104 is disposed on the side of the settling basin 100, and the water W is rectified and flows through the rectifying wall 104. The water flowing into the inflow chamber 103 flows into the lower end inflow portion of the inclined plate or inclined pipe settling device 101. In the inclined plate or inclined tube settling device 101, the incoming water is separated into solid and liquid, and the water rises and flows into the water collecting trough 102. Sludge in the running water is separated in the inclined plate or inclined tube settling device 101, slides down the inclined surface, sinks the inflow chamber 103, and accumulates at the bottom of the inflow chamber 103. The accumulated flocs, that is, sludge, are raked up by the sludge scraper 108 and collected in the sludge pit 105. By opening the mud valve 106, the sludge in the mud pit 105 is discharged out of the sedimentation basin 100. In addition, 107 of FIG. 1 is a drive device which drives the sludge scraper 108.
Water Supply Facility Design Guidelines 2000, 197 pages, issued on March 31, 2000 Japan Water Works Association

図2に示すように水Wは整流壁104を通して均一な流速の整流水wとなって流入室103に流入するが、傾斜板又は傾斜管沈降装置101内においては、沈殿池100に流入する水Wの高濁度による濁度密度流、沈殿池100内の水温差による温度密度流によって傾斜板又は傾斜管沈降装置101内の水の流速が不均一となり(例えば図2のA部分で流速が速くなる)、沈殿池100内のフロックがキャリオーバして後段のろ過池(図示せず)に流出することがある。   As shown in FIG. 2, the water W flows into the inflow chamber 103 as rectified water w having a uniform flow rate through the rectifying wall 104, but the water flowing into the settling basin 100 in the inclined plate or inclined pipe settling device 101. The turbidity density flow due to the high turbidity of W and the temperature density flow due to the water temperature difference in the sedimentation basin 100 cause the water flow rate in the inclined plate or inclined tube settling device 101 to be non-uniform (for example, the flow rate in part A in FIG. The floc in the sedimentation basin 100 may carry over and flow out to a subsequent filtration basin (not shown).

本発明は上述の点に鑑みてなされたもので、傾斜板又は傾斜管沈降装置内に流入する水の流速を均一化して、濁度密度、温度密度流を防止し、沈澱池内のフロックのキャリオーバを防止できる沈殿池設備を提供することを目的とする。 The present invention has been made in view of the above points. The flow rate of water flowing into the inclined plate or inclined tube settling device is made uniform to prevent turbidity density and temperature density flow, and the floc key in the settling basin is prevented. An object is to provide a sedimentation basin facility that can prevent a overflow.

上記課題を解決するため請求項1に記載の発明は、沈澱池内に傾斜板又は傾斜管沈降装置を配置し、傾斜板又は傾斜管沈降装置の上部に集水トラフ、下部に水が流入する流入室を配置すると共に、該流入室底部に堆積した汚泥を排出する汚泥排出機構を備え、該流入室に流入した水が傾斜板又は傾斜管沈降装置を通って集水トラフに流出するように構成した沈澱池設備において、流入室内の傾斜板又は傾斜管沈降装置の下方に該傾斜板又は傾斜管沈降装置に流入する水を整流し且つ汚泥を排出する整流排泥装置を設け、整流排泥装置は、平面状に互いに隣接して配列した多数の整流排泥セルを備え、各整流排泥セルは平断面形状が多角形状で、上端から下方所定位置までの平断面が同じ形状で且つ同じ断面積であり、該断面所定位置から下方はその断面が徐々に縮小するように構成され、下端開口部が水の流入口、上端開口部が水の流出口となっていることを特徴とする。 In order to solve the above-mentioned problem, the invention according to claim 1 is arranged such that an inclined plate or an inclined pipe settling device is disposed in a settling basin, and a water collecting trough is introduced into the upper portion of the inclined plate or the inclined tube settling device, and water flows into the lower portion. with placing the chamber, provided with a sludge discharge mechanism for discharging the sludge deposited on the flow entry bottom, water that has flowed into the flow entry is through the inclined swash plate or inclined tube settler to flow out to the water collecting trough in the configuration the sedimentation tank facilities, provided a rectifying waste sludge device for discharging the inclined plate or inclined tube settler rectifies and sludge water flowing into below the inclined swash plate or inclined tube settler of inflows chamber, rectifier The mud draining device includes a number of rectifying and draining cells arranged adjacent to each other in a planar shape, and each rectifying and draining cell has a polygonal cross-sectional shape and the same cross-sectional shape from the upper end to a predetermined position below. And the same cross-sectional area, the cross-section below the predetermined position Is configured in cross section gradually reduced, the inlet of the lower end opening is water, the upper end opening, characterized in that it is and the outlet of water.

請求項に記載の発明は、請求項1に記載の沈澱池設備において、傾斜板又は傾斜管沈降装置は沈澱池の上下方向所定位置に設置された架台に搭載設置されており、整流排泥装置はその上端が架に傾斜板又は傾斜沈降装置の下方に位置するように取り付けられていることを特徴とする。 The invention according to claim 2, in sedimentation tank installation according to claim 1, inclined swash plate or inclined tube settler is mounted installed to the frame placed in the vertical direction by a predetermined position of the precipitation sediment pond, rectification desludging device is characterized in that its upper end is mounted so as to be positioned below the inclined swash plate or inclined settler to rack mount.

請求項に記載の発明は、請求項1に記載の発明において、整流排泥装置は、その上端が傾斜板又は傾斜管沈降装置の下端に連結し一体的に設けられていることを特徴とする。 Invention according to claim 3, in the invention described in claim 1, integer Nagarehai mud device, that is provided integrally with its upper end connected to the lower end of the inclined swash plate or inclined tube settler Features.

請求項1に記載の発明によれば、各整流排泥セルは平断面形状が多角形状で、上端から下方所定位置までの平断面が同じ形状で且つ同じ断面積であり、該断面所定位置から下方はその断面が徐々に縮小するように構成され、下端開口部が水の流入口、上端開口部が水の流出口となっているので、各整流排泥セルの断面縮小部の下端の流入口に流入する噴流水は断面積が徐々に大きくなっていく部分を通り、断面形状及び断面積が同一部分を通る間に流速が均一化され、傾斜板又は斜管沈降装置下端の流入部に流入する水の流速は均一化され、濁度密度流、温度密度流を防止して沈澱池内のフロックのキャリオーバを防止できる沈澱池設備を提供できる。また、整流排泥装置の各整流排泥セルの平断面形状は正多角形であることが好ましく、さらに矩形状又は正六角形であることがより好ましい。矩形状(正方形)又は正六角形の形状を採用することで、沈澱設備への整流排泥セルの設置が容易になり、また、流入した水の流速がより均一化されやすいからである。 According to the first aspect of the present invention, each rectifying and drainage cell has a polygonal cross-sectional shape, the same cross-sectional area from the upper end to the lower predetermined position, and the same cross-sectional area. The lower part is configured so that its cross section gradually shrinks, the lower end opening is the water inlet, and the upper end opening is the water outlet. jet water flowing into the inlet passes through a portion where the sectional area gradually increases, the uniform flow rate while the cross-sectional shape and cross-sectional area passes through the same portion, inclined swash plate or inlet of the oblique tube settler bottom The flow rate of water flowing into the basin can be made uniform, and turbidity density flow and temperature density flow can be prevented to provide a sedimentation basin facility capable of preventing carryover of flocs in the sedimentation basin. Moreover, it is preferable that the plane cross-sectional shape of each rectification | suction drainage cell of a rectification | straining sludge apparatus is a regular polygon, and it is more preferable that it is a rectangular shape or a regular hexagon. By adopting a rectangular (square) or regular hexagonal shape, it is easy to install the rectification / drainage cell in the sedimentation facility, and the flow rate of the inflowing water is more easily made uniform.

請求項に記載の発明によれば、整流排泥装置を傾斜板又は傾斜管沈降装置が搭載されている架台に該傾斜板又は傾斜管沈降装置の下方に位置するように取り付けたので、傾斜板又は傾斜管沈降装置を架台に搭載させた既存の沈殿池設備を本発明に係る沈殿池設備に容易に改造することができる。 According to the second aspect of the present invention, the rectifying and draining device is attached to the mount on which the inclined plate or the inclined tube settling device is mounted so as to be positioned below the inclined plate or the inclined tube settling device. The existing sedimentation basin equipment in which the plate or the inclined pipe sedimentation device is mounted on the mount can be easily modified to the sedimentation basin equipment according to the present invention.

請求項に記載の発明によれば、整流排泥装置は該傾斜板又は傾斜管沈降装置の下端に一体的に連結されて設けられているので、整流排泥装置と該傾斜板又は傾斜管沈降装置は一体となるから、沈殿池設備の沈殿池への設置が容易となる。

According to the third aspect of the present invention, since the rectifying and draining device is integrally connected to the lower end of the inclined plate or the inclined tube settling device, the rectifying and discharging device and the inclined plate or the inclined tube are provided. Since the settling device is integrated, it is easy to install the settling basin equipment in the settling basin.

以下、本発明の実施の形態例を図面に基いて説明する。図3及び図4は本発明に係る沈殿池設備の沈殿池の要部を示す図で、図3は沈殿池の要部を示す側断面図、図4は図3のB−B平断面図である。沈殿池10内に傾斜板又は傾斜管沈降装置11を配置し、傾斜板又は傾斜管沈降装置11の上部に集水トラフ12、下部に水(濁水)が流入する流入室13を配置している点は、図1の沈殿池設備と同一である。ここでは、流入室13内の傾斜板又は傾斜管沈降装置11の下方に該傾斜板又は傾斜管沈降装置11に流入する水を整流し且つ汚泥を排出する整流排泥装置14を設けている。なお、整流壁、汚泥掻寄機、排泥ピット等は図1と略同一であるから、その図示は省略する。     Embodiments of the present invention will be described below with reference to the drawings. 3 and 4 are views showing the main part of the settling basin of the settling basin equipment according to the present invention, FIG. 3 is a sectional side view showing the main part of the settling basin, and FIG. It is. An inclined plate or inclined pipe settling device 11 is arranged in the sedimentation basin 10, a water collecting trough 12 is arranged at the upper part of the inclined plate or inclined pipe settling device 11, and an inflow chamber 13 into which water (turbid water) flows is arranged at the lower part. The point is the same as the sedimentation basin equipment of FIG. Here, a rectifying and draining device 14 that rectifies water flowing into the inclined plate or inclined pipe settling device 11 and discharges sludge is provided below the inclined plate or inclined pipe settling device 11 in the inflow chamber 13. The flow straightening wall, the sludge scraper, the waste pit, etc. are substantially the same as those in FIG.

整流排泥装置14は互い隣接して平面状に配列した多数の整流排泥セル15を備え、各整流排泥セル15は図5及び図6に示すように、平断面形状が矩形状(正方形)で、上端から下方所定位置まで(上端から下方寸法L4-1まで)はその平断面が同じ矩形状で且つその断面積も同じである。該所定位置から下端まで(寸法L4-1の下端から寸法L4-2まで)その断面が徐々に収縮する収縮部(傾斜部15c)ように構成され、その内面が傾斜面をなしている。即ち、各整流排泥セル15から所定位置までは平断面が矩形状で且つ断面積が同一で、所定位置から下端までが平断面が矩形状で断面積が徐々に収縮するように構成されている。そして整流排泥セル15の下端は開口し水の流入口15aとなっており、上端は同じく開口し水の流出口15bとなっている。ここで、流入口15aから流入する水の噴流を減衰させるためには、開口面積率(流出口15bに対する流入口15a)を5%〜10%程度とするか、または、流入口15aへの流入速度を500mm/min〜200mm/min程度とするのか好ましい。 The rectification / drainage device 14 includes a number of rectification / drainage cells 15 arranged in a plane adjacent to each other, and each of the rectification / drainage cells 15 has a rectangular cross section (square shape) as shown in FIGS. ) From the upper end to a predetermined position below (from the upper end to the lower dimension L 4-1 ), the flat cross section is the same rectangular shape and the cross sectional area is also the same. From the predetermined position to the lower end (from the lower end of dimension L 4-1 to dimension L 4-2 ), the cross section is configured to be a contracted portion (inclined portion 15c) that gradually contracts, and the inner surface forms an inclined surface. . That is, each rectification / drainage cell 15 has a rectangular cross section and the same cross-sectional area from the predetermined position to the predetermined position, and a rectangular cross section from the predetermined position to the lower end and the cross-sectional area gradually contracts. Yes. And the lower end of the rectification mud cell 15 opens and becomes the inflow port 15a of water, and the upper end opens similarly and becomes the outflow port 15b of water. Here, in order to attenuate the jet of water flowing in from the inflow port 15a, the opening area ratio (inlet 15a with respect to the outflow port 15b) is set to about 5% to 10%, or inflow to the inflow port 15a. It is preferable to set the speed to about 500 mm / min to 200 mm / min.

各整流排泥セル15は例えば樹脂材で形成されている。複数個の整流排泥セル15を吊下げ用ワイヤ16で縛り、傾斜板又は傾斜管沈降装置11を設置している架台17に吊り下げて、整流排泥装置14の上端、即ち、各整流排泥セル15の上端開口の流出口15bが傾斜板又は傾斜管沈降装置11の下方に位置するように取り付ける。これにより、既存の沈殿池設備の沈殿池10の流入室13内に整流排泥装置14を配置することが容易となる。即ち、既存の傾斜板又は傾斜管沈降装置11が架台17に設置されている構成の沈殿池設備を本発明に係る沈殿池設備に改造することが容易となる。また、傾斜板又は傾斜管沈降装置11上端から集水トラフ12までの寸法L1、傾斜板又は傾斜管沈降装置11の厚さ寸法L2、傾斜板又は傾斜管沈降装置11下端から整流排泥装置14上端までの寸法L3、整流排泥装置14の厚さ寸法L4は、流速の均一化、フロックの分離、沈降効率等を考慮して任意に設定できるが、ここではL1=600mm、L2=800mm、L3=300mm、L4=500mmとした。 Each rectification mud cell 15 is formed of a resin material, for example. A plurality of rectifying mud cells 15 are bound with suspension wires 16 and hung on a gantry 17 on which an inclined plate or inclined pipe settling device 11 is installed. It attaches so that the outflow port 15b of the upper end opening of the mud cell 15 may be located below the inclined plate or inclined tube settling device 11. Thereby, it becomes easy to arrange the rectifying and draining device 14 in the inflow chamber 13 of the settling basin 10 of the existing settling basin equipment. That is, it becomes easy to remodel the sedimentation basin equipment of the structure in which the existing inclined plate or the inclined pipe sedimentation apparatus 11 is installed on the mount 17 to the sedimentation basin equipment according to the present invention. In addition, the dimension L 1 from the upper end of the inclined plate or inclined pipe settling device 11 to the water collecting trough 12, the thickness dimension L 2 of the inclined plate or inclined pipe settling device 11, the rectified waste mud from the lower end of the inclined plate or inclined pipe settling device 11 The dimension L 3 up to the upper end of the apparatus 14 and the thickness dimension L 4 of the rectifying and draining apparatus 14 can be arbitrarily set in consideration of uniform flow velocity, floc separation, sedimentation efficiency, etc. Here, L 1 = 600 mm L 2 = 800 mm, L 3 = 300 mm, and L 4 = 500 mm.

上記のように互い隣接して平面状に配列した多数の整流排泥セル15で構成された整流排泥装置14において、図6に示すように、各整流排泥セル15の流入口15aから流入した水wは上向に流れる。そして断面積が大きくなった断面拡張部で流速が均一化され、傾斜板又は傾斜管沈降装置11へと流入する。流入する水と共に流入してくるフロック(汚泥)fは整流排泥セル15内で沈降し、下部傾斜部分15cに堆積し、徐々に落下していく。また、傾斜板又は傾斜管沈降装置11から落下するフロックも整流排泥セル15内を沈降し、下部傾斜部分15cに沈降して堆積し徐々に落下していく。この下部傾斜部分15cの傾斜角度θは安息角度に近い角度、即ち50°〜70°好ましくは55°〜65°、より好ましくは60°とするのがよい。また、整流排泥セル15の高さ幅寸法は流入口(下端開口)15aから流入する水の噴流が減衰するのに要する距離に設定する。ここでは高さ寸法L4=500mmとし、断面拡張部の高さ寸法L4-1=200mm、断面収縮部の高さ寸法幅寸法L4-2=300mm、流出口(上端開口)15bの幅寸法L5=500mm、流入口(下端開口)15aの幅寸法L6=150mmとした。 As shown in FIG. 6, in the rectification / drainage device 14 composed of a large number of rectification / drainage cells 15 arranged in a plane adjacent to each other as described above, an inflow is made from the inlet 15 a of each rectification / drainage cell 15. The water w that flows is flowing upward. Then, the flow velocity is made uniform at the cross-section expanded portion where the cross-sectional area is increased, and flows into the inclined plate or inclined pipe settling device 11. The flock (sludge) f that flows in with the inflowing water settles in the rectification / drainage cell 15, accumulates in the lower inclined portion 15c, and gradually falls. In addition, flocs falling from the inclined plate or inclined tube settling device 11 settle in the rectifying / drainage cell 15 and settle on the lower inclined portion 15c and gradually fall. The inclination angle θ of the lower inclined portion 15c is an angle close to the repose angle, that is, 50 ° to 70 °, preferably 55 ° to 65 °, more preferably 60 °. Moreover, the height width dimension of the rectification mud discharge cell 15 is set to the distance required for the jet of water flowing in from the inflow port (lower end opening) 15a to attenuate. Here, the height dimension L 4 = 500 mm, the height dimension L 4-1 = 200 mm of the cross-section expansion part, the height dimension width dimension L 4-2 = 300 mm of the cross-section contraction part, and the width of the outlet (upper end opening) 15b The dimension L 5 = 500 mm and the width dimension L 6 of the inflow port (lower end opening) 15 a was set to 150 mm.

なお、上記例では、整流排泥装置14を傾斜板又は傾斜管沈降装置11とは別々に製造し、複数個の整流排泥セル15からなる整流排泥装置14を吊下げ用ワイヤ16で傾斜板又は傾斜管沈降装置11を設置している架台17に吊り下げて取り付ける例を示したが、これに限定されるものではなく、例えば図7に示すように整流排泥装置14と傾斜板又は傾斜管沈降装置11を一体的に製造し、これを沈殿池に設置するようにしてもよい。これにより、傾斜板又は傾斜管沈降装置11と整流排泥装置14は一体となっているから、沈殿池に設置するのが容易となる。   In the above example, the straightening / mudging device 14 is manufactured separately from the inclined plate or the inclined pipe settling device 11, and the straightening / mudging device 14 composed of a plurality of straightening / mudging cells 15 is inclined by the suspension wire 16. Although the example which suspended and attached to the mount 17 which has installed the board or the inclined pipe sedimentation apparatus 11 was shown, it is not limited to this, For example, as shown in FIG. The inclined pipe settling device 11 may be manufactured integrally and installed in a settling basin. As a result, the inclined plate or inclined pipe settling device 11 and the rectifying and draining device 14 are integrated, so that it is easy to install in the settling basin.

また、整流排泥セル15の形状も平断面矩形に限定されるものではなく、例えば図8(a)、(b)にその平面、側面を示すように、平断面が正六角形で下部に断面が収縮した傾斜部15cを形成し、下端開口部を流入口15a、上端開口部を流出口15bとした整流排泥セル15を用い、この整流排泥セル15を図9(図3のB−B断面に相当)に示すように、多数互い隣接させて平面状に配列して整流排泥装置14を構成してもよい。   Further, the shape of the rectification / drainage cell 15 is not limited to a rectangular rectangular cross section. For example, as shown in FIGS. Is formed, and the rectified waste mud cell 15 having the lower end opening as the inflow port 15a and the upper end opening as the outflow port 15b is used. As shown in (corresponding to the B cross section), the rectifying and discharging apparatus 14 may be configured by arranging a large number of them adjacent to each other in a plane.

以上、本発明の実施形態を説明したが、本発明は上記実施形態に限定されるものではなく、特許請求の範囲、及び明細書と図面に記載された技術的思想の範囲内において種々の変形が可能である。     Although the embodiments of the present invention have been described above, the present invention is not limited to the above-described embodiments, and various modifications can be made within the scope of the technical idea described in the claims and the specification and drawings. Is possible.

従来の沈殿池設備の構成例を示す図である。It is a figure which shows the structural example of the conventional sedimentation basin equipment. 従来の沈殿池設備の水の流れ状態を示す図である。It is a figure which shows the flow state of the water of the conventional sedimentation basin equipment. 本発明に係る沈殿池設備の要部構成例を示す図である。It is a figure which shows the principal part structural example of the sedimentation basin equipment which concerns on this invention. 図3のB−B断面図である。It is BB sectional drawing of FIG. 本発明に係る沈殿池設備の一部を示す図である。It is a figure which shows a part of sedimentation tank installation which concerns on this invention. 本発明に係る沈殿池設備の整流排泥装置の整流排泥セルの水及びフロックの動きを説明するための図である。It is a figure for demonstrating the motion of the water of the rectification | suction mud cell of the rectification / sludge apparatus of the sedimentation basin equipment which concerns on this invention, and a flock. 本発明に係る沈殿池設備の傾斜板又は傾斜管沈降装置及び整流排泥装置の構成例を示す図である。It is a figure which shows the structural example of the inclined plate of the sedimentation basin equipment which concerns on this invention, or an inclined pipe sedimentation apparatus, and a rectification | straightening sludge apparatus. 本発明に係る沈殿池設備の整流排泥装置の整流排泥セルの構成例を示す図である。It is a figure which shows the structural example of the rectification | suction mud cell of the rectification / sludge apparatus of the sedimentation basin equipment which concerns on this invention. 本発明に係る沈殿池設備の整流排泥装置の平面構成例を示す図である。It is a figure which shows the example of a plane structure of the rectification | suction drainage apparatus of the sedimentation basin equipment concerning this invention.

符号の説明Explanation of symbols

10 沈殿池
11 傾斜板又は傾斜管沈降装置
12 集水トラフ
13 流入室
14 整流排泥装置
15 整流排泥セル
16 吊り下げ用ワイヤ
17 架台
10 Sedimentation basin 11 Inclined plate or inclined tube settling device
12 Catchment trough
13 Inflow chamber
14 Rectification drainage device 15 Rectification drainage cell 16 Suspension wire 17 Mount

Claims (3)

沈澱池内に傾斜板又は傾斜管沈降装置を配置し、傾斜板又は傾斜管沈降装置の上部に集水トラフ、下部に水が流入する流入室を配置すると共に、該流入室底部に堆積した汚泥を排出する汚泥排出機構を備え、該流入室に流入した水が前記傾斜板又は傾斜管沈降装置を通って前記集水トラフに流出するように構成した沈澱池設備において、
前記流入室内の前記傾斜板又は傾斜管沈降装置の下方に該傾斜板又は傾斜管沈降装置に流入する水を整流し且つ汚泥を排出する整流排泥装置を設け
前記整流排泥装置は、平面状に互いに隣接して配列した多数の整流排泥セルを備え、
前記各整流排泥セルは平断面形状が多角形状で、上端から下方所定位置までの平断面が同じ形状で且つ同じ断面積であり、該断面所定位置から下方はその断面が徐々に縮小するように構成され、下端開口部が水の流入口、上端開口部が水の流出口となっていることを特徴とする沈澱池設備。
An inclined plate or inclined pipe settling device is arranged in the settling basin, a water collection trough is arranged at the upper part of the inclined plate or inclined pipe settling device, an inflow chamber into which water flows in is arranged at the lower part, and the sludge accumulated at the bottom of the inflow chamber is disposed. In a sedimentation basin facility comprising a sludge discharge mechanism for discharging, and configured such that water flowing into the inflow chamber flows out to the water collection trough through the inclined plate or the inclined pipe settling device,
A rectifying and draining device for rectifying water flowing into the inclined plate or inclined pipe settling device and discharging sludge is provided below the inclined plate or inclined pipe settling device in the inflow chamber ,
The rectifying and draining device includes a large number of rectifying and discharging cells arranged adjacent to each other in a plane,
Each of the rectifying and drainage cells has a polygonal cross-sectional shape, the same cross-sectional area from the upper end to a predetermined position below the upper end, and the same cross-sectional area. A sedimentation basin facility characterized in that the lower end opening is a water inlet and the upper end opening is a water outlet .
請求項1に記載の沈澱池設備において、
前記傾斜板又は傾斜管沈降装置は前記沈澱池の上下方向所定位置に設置された架台に搭載設置されており、
前記整流排泥装置はその上端が前記架台に前記傾斜板又は傾斜沈降装置の下方に位置するように取り付けられていることを特徴とする沈澱池設備。
In the settling pond facility according to claim 1 ,
The inclined plate or the inclined pipe settling device is mounted on a base installed at a predetermined position in the vertical direction of the settling pond,
The rectifying and drainage device is attached to the gantry so that its upper end is positioned below the inclined plate or inclined settling device.
請求項1に記載の沈澱池設備において、
前記整流排泥装置は、その上端が前記傾斜板又は傾斜管沈降装置の下端に連結し一体的に設けられていることを特徴とする沈澱池設備。
In the settling pond facility according to claim 1 ,
The rectifier waste sludge system, sedimentation basin equipment, characterized in that the upper end is linked integrally provided on the lower end of the front Ki傾 swash plate or inclined tube settler.
JP2005262181A 2005-09-09 2005-09-09 Sedimentation basin equipment Expired - Fee Related JP4537917B2 (en)

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JPS52116650A (en) * 1976-03-24 1977-09-30 Degremont Water treatment apparatus and method
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JPS56137704U (en) * 1980-03-17 1981-10-19
JPS61136407A (en) * 1984-12-07 1986-06-24 Waseda Giken Kk Upwardly flowing type inclined sedimentation basin
JPS62298409A (en) * 1986-06-19 1987-12-25 Waseda Giken Kk Upward flow type inclined settling pond
JPS63274411A (en) * 1986-05-07 1988-11-11 デグレマン Lamelar decanter
JPH08912A (en) * 1994-06-17 1996-01-09 Asahi Tec Corp Sedimentation separation apparatus
JPH10511167A (en) * 1995-05-26 1998-10-27 ハリス,ロナルド・ビー Linear solids remover
JP2001187303A (en) * 2000-01-05 2001-07-10 Yoshiji Sakamoto Solid-liquid separator in wastewater treatment equipment

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JPS4921473U (en) * 1972-05-26 1974-02-23
JPS4989253A (en) * 1972-12-28 1974-08-26
JPS51117361A (en) * 1975-04-09 1976-10-15 Hitachi Metals Ltd Sedimentation and separation oblique plate
JPS52116650A (en) * 1976-03-24 1977-09-30 Degremont Water treatment apparatus and method
JPS5467267A (en) * 1977-11-09 1979-05-30 Miura Eng Internatl Kk Slurry settling separator
JPS56137704U (en) * 1980-03-17 1981-10-19
JPS61136407A (en) * 1984-12-07 1986-06-24 Waseda Giken Kk Upwardly flowing type inclined sedimentation basin
JPS63274411A (en) * 1986-05-07 1988-11-11 デグレマン Lamelar decanter
JPS62298409A (en) * 1986-06-19 1987-12-25 Waseda Giken Kk Upward flow type inclined settling pond
JPH08912A (en) * 1994-06-17 1996-01-09 Asahi Tec Corp Sedimentation separation apparatus
JPH10511167A (en) * 1995-05-26 1998-10-27 ハリス,ロナルド・ビー Linear solids remover
JP2001187303A (en) * 2000-01-05 2001-07-10 Yoshiji Sakamoto Solid-liquid separator in wastewater treatment equipment

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